Low Pressure Mixing System for Desalting Hydrocarbons
A method and system for reducing the salt content of a crude oil stream includes using a quill to disperse a water stream into the crude oil and then routing the mixed oil/water stream through a plurality of mixing stages. The water stream may include a wash water that has been preconditioned with recycled effluent water. Each mixing stage increases the homogeneity of the mixed oil/water stream. The first and third mixing stages are preferably lower pressure stages relative to the second mixing stage, which provides pressure effective for flowing the mixed oil/water stream through the third and fourth mixing stages. Upon exiting the fourth mixing stage, the mixed oil/water stream is electrostatically treated in a dual frequency separator vessel or a dual polarity separator vessel.
1 . A method for use in reducing a salt content of a crude oil stream comprising the steps of:
dispersing a water stream into the crude oil stream to produce a mixed oil/water stream;
routing the mixed oil/water stream through a plurality of mixing stages to increase the homogeneity of the mixed oil/water stream;
routing the mixed oil/water stream to a separator vessel whereby at least a substantial portion of said salt content is absorbed by water in said mixed stream;
electrostatically treating said mixed oil/water stream in said separator vessel;
extracting water from a lower portion of said separator vessel; and
extracting treated oil from an upper portion of said separator vessel.
2 . A method according to claim 1 wherein at least one of said mixing stages has a pressure differential in a range of 3 to 5 psi.
3 . A method according to claim 1 wherein at least one of said mixing stages has a pressure differential of about 25 psi.
4 . A method according to claim 1 wherein said mixing stages includes a boost pump.
5 . A method according to claim 1 wherein one of said mixing stages has a pressure differential in a range of 5 to 20 psi.
6 . A method according to claim 1 including the step of preconditioning said water stream with an effluent water stream.
7 . A method according to claim 1 including the step of recycling a portion of the water extracted from said separator vessel into said water stream to produce said mixed oil/water stream.
8 . A method according to claim 1 wherein said plurality of mixing stages includes a first, second, third and fourth mixing stage and wherein each mixing stage increases the homogeneity of said mixed oil/water stream.
9 . A method according to claim 1 wherein said step of electrostatically treating said mixed oil/water stream in said separator vessel uses a separation vessel selected from a dual polarity electrostatic separator vessel and a dual frequency electrostatic separator vessel.
10 . A method according to claim 1 further comprising the step of adding a wetting agent to the water stream.
11 . A system for desalting hydrocarbons comprising:
a crude oil stream;
a water stream;
a quill;
a first, second, third and fourth mixing stage;
a separator vessel located downstream of said fourth mixing stage;
said separator vessel being selected from the group consisting of a dual frequency electrostatic separator vessel and a dual polarity electrostatic separator vessel;
each said mixing stage being effective for increasing the homogeneity of a mixed oil/water stream;
said first and third mixing stages including a static mixer and each being a lower pressure mixing stage relative to the second mixing stage;
said second mixing stage providing a pressure increase effective for flowing the mixed oil/water stream through the third and fourth mixing stages;
said fourth mixing stage including a mixing valve and being capable of providing increased mix energy relative to said third mixing stage.
12 . A system according to claim 11 further comprising the water stream including a wash water and an effluent water.
13 . A system according to claim 12 further comprising a water mixing stage including a static mixer.
14 . A system according to claim 11 further comprising at least one of said first and third mixing stages having a pressure differential in a range of 3 to 5 psi.
15 . A system according to claim 11 further comprising said second mixing stage including a boost pump.
16 . A system according to claim 11 further comprising said second mixing stage having a pressure differential of about 25 psi.
17 . A system according to claim 11 further comprising said fourth mixing stage having a pressure differential in a range of 5 to 20 psi.
18 . A system according to claim 11 further comprising a bypass piping for bypassing said first and second mixing stages.
19 . A system according to claim 11 further comprising the water stream including a wetting agent.